JPS5875603A - Combustion method for solid matter - Google Patents

Combustion method for solid matter

Info

Publication number
JPS5875603A
JPS5875603A JP17210681A JP17210681A JPS5875603A JP S5875603 A JPS5875603 A JP S5875603A JP 17210681 A JP17210681 A JP 17210681A JP 17210681 A JP17210681 A JP 17210681A JP S5875603 A JPS5875603 A JP S5875603A
Authority
JP
Japan
Prior art keywords
solid
fuel
solids
powdery
fed
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP17210681A
Other languages
Japanese (ja)
Inventor
Seiichi Takahashi
清一 高橋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP17210681A priority Critical patent/JPS5875603A/en
Publication of JPS5875603A publication Critical patent/JPS5875603A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23BMETHODS OR APPARATUS FOR COMBUSTION USING ONLY SOLID FUEL
    • F23B5/00Combustion apparatus with arrangements for burning uncombusted material from primary combustion
    • F23B5/02Combustion apparatus with arrangements for burning uncombusted material from primary combustion in main combustion chamber

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Solid-Fuel Combustion (AREA)

Abstract

PURPOSE:To efficiently and stably burn unburnt portion contained in a solid fuel, by adding powdery asphalt to powdery solid to mix with it after unburnt solid is collected, and by binding them into a lump to burn by acting a heating fluid. CONSTITUTION:Bulky solid in a solid fuel is separated from powdery solid by a classifier 8, fed into a fuel feeder 2 through a conveying means 9, and is fed into a combustion furnace 1 by the fuel feeder 2. On one hand, powdery solid is fed into a powdery fuel mixer 7 through a conveying means 10. While, unburnt solid matter in exhaust gas discharged from the combustion furnace 1 is collected by an unburnt solid catcher 4, and is fed also into the powdery fuel mixer 7 by a conveying means 5. Then, heating fluid is fed into a heating unit 11, passing through a heating fluid passage 13, heating the inside of a heating unit 11, where powdery asphalt is melted to be bound with powdery unburnt coal which is fed from the powdery fuel mixer 7. By this method, volatile component in the asphalt is added to the unburnt solid, as a result, the quality of solid as a fuel is improved, and unburnt loss of the fuel is decreased.

Description

【発明の詳細な説明】 本発明は、燃焼炉、例えはストーカ焚き燃焼炉、#L!
I7I床炉等で石炭、木片、ピッチ、プラスチック等の
固形物を燃焼させる固形物燃焼方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides a combustion furnace, for example a stoker-fired combustion furnace, #L!
This invention relates to a method for burning solid materials such as coal, wood chips, pitch, and plastics in an I7I floor furnace.

従来の燃焼方法を第1図に示す態様例にカFづいて説明
する。
A conventional combustion method will be explained with reference to the embodiment shown in FIG.

燃焼炉0’ 1には塊状固形物、粉状固形物の燃料07
を燃焼炉01内に供給する燃料供給装置02が設けられ
、燃焼炉01の排ガス08の出口に設けられたダクト0
3の途中には未燃固形物捕集装置04が設けられている
。未燃固形物捕集装置04の未燃固形物出口には、未燃
固形物を燃焼炉01内に導く輸送手段05が連結されて
いる。又、燃焼炉01は、燃焼炉01に燃・焼用空気0
9を供給するための送風機06と連通している。
Combustion furnace 0' 1 contains lumpy solids and powdered solids as fuel 07
A duct 0 is provided at the outlet of the exhaust gas 08 of the combustion furnace 01.
An unburnt solids collection device 04 is provided in the middle of the pipe 3. A transportation means 05 that guides the unburned solids into the combustion furnace 01 is connected to the unburned solids outlet of the unburned solids collection device 04 . In addition, the combustion furnace 01 has 0 air for combustion/combustion in the combustion furnace 01.
It communicates with a blower 06 for supplying air.

燃焼炉01内に燃料供給装置02から塊状固形物の燃料
07を供給し、送風機06を介して供給される燃焼゛用
空気09によって固形物の燃料07゜を燃焼させる。ダ
ク)03内を流れる排ガス08の中に含まれる灰と未燃
唄彫物は未燃固形物捕集装置04で分康し、灰は炉外へ
排出し、未燃固形物は再び輸送手段05を介して燃焼炉
01内に供給され再燃焼する。
A lumpy solid fuel 07 is supplied into the combustion furnace 01 from a fuel supply device 02, and the solid fuel 07 is combusted by combustion air 09 supplied through a blower 06. The ash and unburned song carvings contained in the exhaust gas 08 flowing through the duct) 03 are separated by the unburned solids collection device 04, the ash is discharged outside the furnace, and the unburnt solids are returned to the transportation means 05. The fuel is supplied to the combustion furnace 01 through the combustion chamber 01 and re-combusted.

従来の方法では、回収した未燃固形物を燃焼炉01Ka
しても、完全に燃焼し切らず、未燃分として糸外に持ち
去られ廃棄処理に手間をシして(・た。又燃料供給装置
02から燃・焼炉OL内へ(X i言されろ塊状・固形
物の燃料07の中にも多量の粉状固形物が含まれており
、塊状固形物の混在によって塊状固形物の燃料07のみ
の場合より燃焼しにくく送風機06の動力を太き(する
例かあった。
In the conventional method, the recovered unburned solids are transferred to the combustion furnace 01Ka.
However, the fuel is not completely combusted and is carried away as unburned components outside the thread, making disposal time consuming. The lumpy/solid fuel 07 also contains a large amount of powdery solids, and the mixture of lumpy solids makes it more difficult to burn than when only the lumpy solid fuel 07 is used, increasing the power of the blower 06. (There was an example of that.

そのため粉状固形物を前処理段階で分離してかし塊状固
形物のみを燃料とすることも行なわれている。また燃料
が燃えつきるまでには多数回にわたり、未燃固形物捕集
装置04と燃焼炉010間を循環する必要があるため、
未燃固形物(…集装置04の容量を太き(したり循環系
の目づまりや摩れの対策を講じていた。
Therefore, it is also practiced to separate the powdery solids in a pretreatment stage and use only the lumpy solids as fuel. In addition, since the fuel needs to be circulated between the unburned solids collector 04 and the combustion furnace 010 many times until it is completely burned out,
Measures were taken to prevent clogging and abrasion of the circulation system by increasing the capacity of unburned solids (...collecting device 04).

そこで本発明は、固形物燃料及び燃焼炉から排出される
未燃分を効率よく、かつ安定して燃焼させるための固定
物燃焼方法を提供することを目的としてなされたもので
ある。本発明は、燃・屍炉内に固形物を供給して燃焼さ
せるとともに、炉外に排出される排ガス中の未燃固形物
を回収した後炉内へ供給して再、燃焼させる固形物燃料
の燃焼方法において、 Sir記固形物を塊状固形物と
粉状固形1グとに分離して前記塊状固形物を炉内に供給
して燃焼させるとともに、前記未燃固形物を回収した恢
、これに前記粉状固形物と粉状アスファルトとをh版加
混合し、更に加熱流体を作用させて塊状イヒし炉内へ供
給して燃焼させることを特徴とする固形物燃焼方法を提
供している。
SUMMARY OF THE INVENTION Accordingly, the present invention has been made with the object of providing a method for burning solid materials that efficiently and stably burns solid fuel and unburned matter discharged from a combustion furnace. The present invention provides a solid fuel that supplies solid matter into a combustion/destruction furnace and burns it, collects unburned solid matter in the exhaust gas discharged outside the furnace, and then supplies it into the furnace and burns it again. In the combustion method, the solid material is separated into a lumpy solid material and 1 gram of powdered solid material, and the lumpy solid material is fed into a furnace and burned, and the unburned solid material is recovered. The present invention provides a solid material combustion method characterized in that the powdered solid material and powdered asphalt are added and mixed together, and then a heating fluid is applied to form a lump, which is then fed into a furnace and burned. .

本発明が提供する方法によれは、排ガス中の未燃固形物
と粉状固形物とを粉状アスファルトをブ「し、更に加熱
流体を鎖部へ注入して塊状化して燃焼炉内で燃焼させる
ので、未燃固形物が炉外へ未燃焼のまま排出されないの
で燃焼効率が良く、粉状固形物の減少に伴ない燃焼が安
定化し1機器の容量アンプも不用で、燃料中に粉状固形
物か混在していても効率よく燃焼でき、燃料が完全燃焼
するので、系内の多数回の循環が不用となり、系内の目
づまりや摩耗のトラブルも少なく灰のみか)発棄物とし
て排出されるので廃棄処理が簡単となり、燃料中に多量
の粉状固形物か含まれて〜・ても燃料として使え4!r
m燃料か使用てきる°ようになる等の利点か得られる。
According to the method provided by the present invention, unburned solids and powdered solids in the exhaust gas are blown with powdered asphalt, and heated fluid is further injected into the chain to form agglomerates, which are then burned in a combustion furnace. As a result, unburned solids are not discharged unburned outside the furnace, resulting in good combustion efficiency, combustion is stabilized as powdery solids decrease, and a capacity amplifier for one device is not required. Even if solid matter is mixed in, it can be burned efficiently, and the fuel is completely combusted, so there is no need for multiple circulations in the system, and there is less trouble with clogging and wear in the system, and only ash is used as waste. Since it is discharged, disposal becomes easy, and even if the fuel contains a large amount of powdery solids, it can be used as fuel.
Benefits such as being able to use less fuel can be obtained.

また粉状アスファルトを用いるので、アスファルト輸送
時にアスファルトを加熱して液化するなどの必要もない
Furthermore, since powdered asphalt is used, there is no need to heat the asphalt to liquefy it during transport.

次に本発明を第2図に示す第1の実施態様に基ついて具
体的に説明する。
Next, the present invention will be specifically explained based on the first embodiment shown in FIG.

燃焼炉1には、塊状固形物を燃焼炉l内に供給する燃料
供給装置2か設けられ、燃焼炉lの排ガス出口に連結さ
れたダクト3の途中には未燃固形物捕集装置4が設けら
れている。未燃固形′吻桶束装置4の未燃固形物排出口
には未燃固形物を粉末混合機7内に導(桶送手段5が設
けられている。
The combustion furnace 1 is provided with a fuel supply device 2 that supplies lumpy solids into the combustion furnace 1, and an unburned solids collection device 4 is installed in the middle of a duct 3 connected to the exhaust gas outlet of the combustion furnace 1. It is provided. An unburned solid discharge port of the unburned solid proboscis bucket bundling device 4 is provided with a bucket feeding means 5 for introducing the unburned solid into the powder mixer 7.

固形物を塊状固形物と粉状固形物とに分ける分級器8に
は、塊状固形物排出口から塊状固形物を燃料供給装置2
に導く輸送手段9か設けられ、又分級器8には粉状固形
物を後述の粉末混合機7に青く輸送手段10が設けられ
、粉末混合機7の出口は通路12に設げられて加熱器1
1に通じ、カロ熱器11には加熱流体#c、wj13が
設げられている。
The classifier 8 that separates the solids into lumpy solids and powdery solids has a fuel supply device 2 that supplies the lumpy solids from the lumpy solids discharge port.
The classifier 8 is provided with a transportation means 9 for transporting powdered solids to a powder mixer 7 (to be described later), and a transportation means 10 is provided for transporting the powdered solids to the powder mixer 7, which will be described later.The outlet of the powder mixer 7 is provided in a passage 12 for heating Vessel 1
1, heating fluids #c and wj13 are provided in the Calo heater 11.

又加熱器11の出口には混合物を燃焼炉1円に尋く輸送
手段14が設けられている。さらに燃・焼炉lは、炉内
に燃焼用空気を供給するための送風機6と連通している
Further, at the outlet of the heater 11, there is provided a transport means 14 for transporting the mixture to the combustion furnace. Furthermore, the combustion furnace 1 is in communication with a blower 6 for supplying combustion air into the furnace.

固形物′燃料中の塊状固形物は、分級器8て粉状固形物
と分離され輸送手段9を介して燃料供給装置2に送られ
、燃料供給装置より燃焼炉1へ供給する。一方粉状固形
物は輸送手段10をブrして粉末混合機7へ走られる。
Solids' The lumpy solids in the fuel are separated from powder solids by a classifier 8, sent to the fuel supply device 2 via a transportation means 9, and supplied to the combustion furnace 1 from the fuel supply device. On the other hand, the powdered solids are passed through the transportation means 10 and run to the powder mixer 7.

燃焼炉1からの排ガス中の未燃固形物は未燃固形捕集装
置4で捕集され。
Unburned solids in the exhaust gas from the combustion furnace 1 are collected by an unburned solids collector 4.

輸送手段5により粉末混合機7へ送られる。It is sent to the powder mixer 7 by means of transport 5.

第3図は前述の粉末混合機7および加熱器110部分の
断面図を示し、粉末混合機7に、排ガス中から未燃固形
物捕集装置において捕集した固形物を輸送手段5により
1粒径の細かな粉状固形物を輸送手段lOにより粉砕し
て1 am程度になった全量の6−710%の粉状アス
ファルトを輸送手段16により送り込み、さらに送気管
17かもこの粉末混合機7の中へ常温以下の温度の空気
を吹き込んで攪拌する。余刺窒気は空気抜き18がも放
出する。上記未燃分や粉状の燃料を粉状アス7アルトと
充分混合後粉末混合機7の底部の仕切板へ19と、加熱
器8部の仕切板B20を開き加熱器1】に移送後、加熱
器11の上部の仕切板B20を閉じる。
FIG. 3 shows a cross-sectional view of the powder mixer 7 and the heater 110, in which solids collected from the exhaust gas by the unburned solids collector are transferred into the powder mixer 7 by means of transport 5. Powdered solids with a fine diameter are pulverized by the transportation means 1O, and 6-710% of the total amount of powdered asphalt, which is about 1 am, is sent by the transportation means 16, and the air pipe 17 is also connected to the powder mixer 7. Air at a temperature below room temperature is blown into the mixture and stirred. The residual nitrous air is also released by the air vent 18. After thoroughly mixing the unburned content and powdered fuel with the powdered Asu7 Alto, transfer it to the partition plate 19 at the bottom of the powder mixer 7, and then open the partition plate B20 of the heater 8 section and transfer it to the heater 1. The partition plate B20 at the top of the heater 11 is closed.

次に温度が粉状アスファルトの軟化点より光分尚く、通
常150°C程度の温度の排ガス等の力り熱流体9を加
熱流体流路13の入口13aから送り加熱器ll内を加
温して粉状アスファル) y−cとかし粉状の未燃分や
石炭と結合する。加熱流体は加熱υIC体出口13bか
ら放出する。粉状の未燃分や石炭がアスファルトと結合
してから加熱流体を止め、力n熱器11内の温度がアス
ファルトの軟化点以下になってから加熱器11の底部の
仕切板C21を開き塊状になった固形物燃料を受取板2
2から取り出す。
Next, a thermal fluid 9 such as exhaust gas, whose temperature is light minutes higher than the softening point of powdered asphalt and usually about 150°C, is sent from the inlet 13a of the heating fluid flow path 13 to heat the inside of the heater 11. Asphalt (powdered asphal) is combined with y-c and powdered unburned matter and coal. The heating fluid is discharged from the heating υIC body outlet 13b. After the powdered unburned content and coal combine with the asphalt, the heating fluid is stopped, and after the temperature inside the heating device 11 becomes below the softening point of the asphalt, the partition plate C21 at the bottom of the heating device 11 is opened to remove the lumps. The solid fuel that has become
Take it out from 2.

このような方法で固形物を燃焼するので、次の効果か得
られる。
By burning solid matter in this way, the following effects can be obtained.

′ア)、 粉末の未燃分にアスファルト中のfすf発成
分が加わり燃料の質が高(なり、完全燃焼する。
'a) The fsf emitting components in the asphalt are added to the unburned content of the powder, resulting in a high quality fuel and complete combustion.

イ)、 燃えにくい粉状未燃分を塊状にすることて、固
定床上で燃焼が可能な燃料になるので熱効率か良い。燃
焼も安定し完全燃焼するので、系内の目づまりや摩耗の
トラブルなども少ない。灰のみが廃棄物として排出され
るので廃棄処理が簡単となる。
B) By turning hard-to-flammable unburned powder into lumps, it becomes a fuel that can be combusted on a fixed bed, so it has good thermal efficiency. Since combustion is stable and complete, there are fewer problems such as clogging or wear within the system. Since only the ash is discharged as waste, disposal becomes easy.

燃料中に多量の粉状固形物が含またていても燃料として
使えるので、各種の燃料が使用できる。
Even if the fuel contains a large amount of powdered solids, it can be used as fuel, so a variety of fuels can be used.

第4図はス1−−力燃焼炉に本発明を適用した第2の実
施例を示すもので加熱流体を力n熱用排ガス流路15か
ら取っていることだけが相異している。
FIG. 4 shows a second embodiment in which the present invention is applied to a thermal combustion furnace, and the only difference is that the heating fluid is taken from the exhaust gas flow path 15 for thermal heat.

すなわち、石炭などの固形物燃料の中の塊状固形物を分
級器8で分離して、燃料供給装置2で燃焼炉1へ供給す
る。分離された粉状固形物は粉末混合機7″へ送る。
That is, lumpy solids in solid fuel such as coal are separated by a classifier 8 and supplied to the combustion furnace 1 by a fuel supply device 2. The separated powder solids are sent to a powder mixer 7''.

排ガス中の未燃固形物は粉状固形物捕集装置4で捕集さ
れ、粉末混合機7へ送る。次に粉状アスファルトを粉末
混合機7へ送り、空気で撹拌混合後、加熱器11へ送り
、排ガスの余熱で加温口て粉状固形物を結合後、できた
塊状燃料を燃焼炉1て燃やす。
Unburned solids in the exhaust gas are collected by a powder solids collector 4 and sent to a powder mixer 7. Next, the powdered asphalt is sent to the powder mixer 7, and after being stirred and mixed with air, it is sent to the heater 11, and the remaining heat of the exhaust gas is used to combine the powdery solids at the heating port, and the resulting lump fuel is sent to the combustion furnace 1. burn.

結局第1実施例とほぼ同様な効果を+1し、アスファル
ト中の揮発成分か、未燃固形物に加わり燃料としての質
が高くなり、未燃損失が低減され、 ゛排ガスの余熱を
利用して粉状アスファルトを粉状固形物に結合できる。
In the end, almost the same effect as in the first embodiment is added, and the volatile components in the asphalt are added to the unburned solids to improve the quality of the fuel, reduce unburned losses, and ``utilize the residual heat of the exhaust gas.'' Powdered asphalt can be combined with powdered solids.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は従来の固形物燃焼方法を実施する装置のフロー
チャート図、第2図は本発明の第1の′太施例のフロー
チャート図、第3図は本発明に使用される粉末混合機お
よび加熱器の実施前体を示す断面図、および第4図は本
発明の第2の実施例のフローチャート図である。 01・・焼却炉、02・・燃料供給装置、03・・ダク
ト、04・・未燃固形捕集装置、05・・輸送手段、0
6・・送風機、07・・粉状固形物の燃料、08・・排
ガス、09・・燃焼用空気、■・・燃焼炉、2・・燃料
供給装置、3・・ダクト、4・・未燃固形物捕集装置、
5・・転送手段。 6・・送風機、7・・粉末混合機、8・・分級器、9、
lO・・輸送手段、11e・加熱器、12・・通路、1
3・・加熱流体流路、14・・輸送手段、15・・加熱
用排ガス流路、16・・輸送手段。 17・・送気管、18・・空気抜き、19,20゜21
・・仕切板A、B、C,22・・受取板。
FIG. 1 is a flowchart of an apparatus for carrying out a conventional solid matter combustion method, FIG. 2 is a flowchart of a first embodiment of the present invention, and FIG. 3 is a flowchart of a powder mixer used in the present invention. FIG. 4 is a sectional view showing a pre-implementation body of the heater, and a flowchart of a second embodiment of the present invention. 01...Incinerator, 02...Fuel supply device, 03...Duct, 04...Unburned solid collection device, 05...Transportation means, 0
6.Blower, 07.Powdered solid fuel, 08.Exhaust gas, 09.Combustion air, ■.Combustion furnace, 2.Fuel supply device, 3.Duct, 4.Unburned solids collector,
5. Transfer means. 6. Blower, 7. Powder mixer, 8. Classifier, 9.
1O...transportation means, 11e-heater, 12...passage, 1
3. Heating fluid flow path, 14. Transportation means, 15. Heating exhaust gas flow path, 16. Transportation means. 17... Air pipe, 18... Air vent, 19, 20° 21
...Partition plates A, B, C, 22... Receiving board.

Claims (1)

【特許請求の範囲】[Claims] 燃焼炉内に固形物を供給して燃焼させるとともに、炉外
に排出される排ガス中の未燃固形物を回収した後炉内へ
供給して再燃焼させる固形?/I燃焼方法において、前
記固形物を塊状固形物と粉状固形物とに分離して、前記
塊状固形物を炉内に供給して燃焼させるとともに、前記
未燃固形物を回収した後これに前記粉状固、彫物と粉状
アスファルトとを添加混合し、更にこれに加熱流体を作
用させて塊状化し、その後炉内へ供給して燃焼させるこ
とを特徴とする固形物燃焼方法。
Solids are fed into the combustion furnace and burned, and unburned solids are recovered from the exhaust gas discharged outside the furnace and then fed into the furnace to be re-burned. /I In the combustion method, the solids are separated into lumpy solids and powdered solids, and the lumpy solids are fed into a furnace and burned, and the unburnt solids are collected and then burned. A method for burning solid materials, which comprises adding and mixing the powdered solids, carvings, and powdered asphalt, and then applying a heating fluid to the mixture to form a lump, and then feeding the mixture into a furnace and burning it.
JP17210681A 1981-10-29 1981-10-29 Combustion method for solid matter Pending JPS5875603A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17210681A JPS5875603A (en) 1981-10-29 1981-10-29 Combustion method for solid matter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17210681A JPS5875603A (en) 1981-10-29 1981-10-29 Combustion method for solid matter

Publications (1)

Publication Number Publication Date
JPS5875603A true JPS5875603A (en) 1983-05-07

Family

ID=15935653

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17210681A Pending JPS5875603A (en) 1981-10-29 1981-10-29 Combustion method for solid matter

Country Status (1)

Country Link
JP (1) JPS5875603A (en)

Similar Documents

Publication Publication Date Title
US4259911A (en) Fluidized bed boiler feed system
US4411204A (en) Method of firing a pulverized fuel-fired steam generator
US5078100A (en) Method and apparatus for burning solid or sludge-like fuels in a fluidized bed
US7273015B2 (en) Method and apparatus for combustion of residual carbon in fly ash
US4856460A (en) Fluidized bed combustion
JPH02290406A (en) Device for gasifying or burning solid carbonaceous material for circulating fluidized bed reactor
CA2266770A1 (en) Process and device for incineration of particulate solids
CZ278704B6 (en) Process and apparatus for combined combustion of coal
US5611935A (en) Method and device for treating sludge
JPS6215600B2 (en)
JPS6021282B2 (en) Powder fuel combustion method
CZ2002999A3 (en) Burning process of biological fuel within a furnace employing fossil fuel
JPS5875603A (en) Combustion method for solid matter
CA1261204A (en) Process for operating a fluidized bed burner
KR960001003B1 (en) Device for calcining cement
JPH0133522B2 (en)
JPS6247474B2 (en)
JPS6246763B2 (en)
JPS5875604A (en) Combustion method for solid matter
JPS62237213A (en) Combustion substance feeding method for fluidized bed heat reaction device and fluidized bed heat reaction device
JPH09178149A (en) Coal ash fluidized bed combustion apparatus and powder mixture supply apparatus in coal ash containing non-combusted component reducing apparatus
RU2799638C1 (en) Technological line for the production of carbonized briquettes based on coal (variants)
JPS5917063B2 (en) Limestone firing method using solid fuel with high volatile content
JPS60501516A (en) How to operate a fluidized bed combustion equipment
JP4105864B2 (en) Recycling method of fly ash in fluidized bed boiler.